Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
288.20 | 0.0500 | 0.2760 |
288.20 | 0.0996 | 0.5130 |
288.20 | 0.1496 | 0.6980 |
288.20 | 0.2011 | 0.8580 |
288.20 | 0.2515 | 0.9890 |
288.20 | 0.3009 | 1.093 |
288.20 | 0.3506 | 1.175 |
288.20 | 0.3988 | 1.25 |
288.20 | 0.4486 | 1.295 |
288.20 | 0.4993 | 1.311 |
288.20 | 0.5500 | 1.319 |
288.20 | 0.5995 | 1.285 |
288.20 | 0.6464 | 1.256 |
288.20 | 0.6980 | 1.18 |
288.20 | 0.7453 | 1.093 |
288.20 | 0.7969 | 0.9780 |
288.20 | 0.8536 | 0.7960 |
288.20 | 0.9030 | 0.5820 |
288.20 | 0.9500 | 0.3350 |
298.20 | 0.0500 | 0.3070 |
298.20 | 0.0996 | 0.5550 |
298.20 | 0.1496 | 0.7630 |
298.20 | 0.2011 | 0.9370 |
298.20 | 0.2515 | 1.083 |
298.20 | 0.3009 | 1.198 |
298.20 | 0.3506 | 1.286 |
298.20 | 0.3988 | 1.361 |
298.20 | 0.4486 | 1.402 |
298.20 | 0.4993 | 1.426 |
298.20 | 0.5500 | 1.435 |
298.20 | 0.5995 | 1.408 |
298.20 | 0.6464 | 1.352 |
298.20 | 0.6980 | 1.272 |
298.20 | 0.7453 | 1.184 |
298.20 | 0.7969 | 1.016 |
298.20 | 0.8536 | 0.7680 |
298.20 | 0.9030 | 0.5860 |
298.20 | 0.9500 | 0.3230 |
313.20 | 0.0500 | 0.3390 |
313.20 | 0.0996 | 0.6100 |
313.20 | 0.1496 | 0.8510 |
313.20 | 0.2011 | 1.042 |
313.20 | 0.2515 | 1.198 |
313.20 | 0.3009 | 1.33 |
313.20 | 0.3506 | 1.434 |
313.20 | 0.3988 | 1.509 |
313.20 | 0.4486 | 1.563 |
313.20 | 0.4993 | 1.58 |
313.20 | 0.5500 | 1.575 |
313.20 | 0.5995 | 1.543 |
313.20 | 0.6464 | 1.486 |
313.20 | 0.6980 | 1.387 |
313.20 | 0.7453 | 1.268 |
313.20 | 0.7969 | 1.086 |
313.20 | 0.8536 | 0.8440 |
313.20 | 0.9030 | 0.6020 |
313.20 | 0.9500 | 0.3010 |
328.20 | 0.0500 | 0.3650 |
328.20 | 0.0996 | 0.6730 |
328.20 | 0.1496 | 0.9260 |
328.20 | 0.2011 | 1.146 |
328.20 | 0.2515 | 1.324 |
328.20 | 0.3009 | 1.459 |
328.20 | 0.3506 | 1.572 |
328.20 | 0.3988 | 1.647 |
328.20 | 0.4486 | 1.703 |
328.20 | 0.4993 | 1.709 |
328.20 | 0.5500 | 1.713 |
328.20 | 0.5995 | 1.657 |
328.20 | 0.6464 | 1.591 |
328.20 | 0.6980 | 1.475 |
328.20 | 0.7453 | 1.321 |
328.20 | 0.7969 | 1.163 |
328.20 | 0.8536 | 0.8930 |
328.20 | 0.9030 | 0.6070 |
328.20 | 0.9500 | 0.1980 |
Operational condition: Pressure, kPa = 101.3 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid |
288.20 | 0.0500 | 0.2760 |
288.20 | 0.0996 | 0.5130 |
288.20 | 0.1496 | 0.6980 |
288.20 | 0.2011 | 0.8580 |
288.20 | 0.2515 | 0.9890 |
288.20 | 0.3009 | 1.093 |
288.20 | 0.3506 | 1.175 |
288.20 | 0.3988 | 1.25 |
288.20 | 0.4486 | 1.295 |
288.20 | 0.4993 | 1.311 |
288.20 | 0.5500 | 1.319 |
288.20 | 0.5995 | 1.285 |
288.20 | 0.6464 | 1.256 |
288.20 | 0.6980 | 1.18 |
288.20 | 0.7453 | 1.093 |
288.20 | 0.7969 | 0.9780 |
288.20 | 0.8536 | 0.7960 |
288.20 | 0.9030 | 0.5820 |
288.20 | 0.9500 | 0.3350 |
298.20 | 0.0500 | 0.3070 |
298.20 | 0.0996 | 0.5550 |
298.20 | 0.1496 | 0.7630 |
298.20 | 0.2011 | 0.9370 |
298.20 | 0.2515 | 1.083 |
298.20 | 0.3009 | 1.198 |
298.20 | 0.3506 | 1.286 |
298.20 | 0.3988 | 1.361 |
298.20 | 0.4486 | 1.402 |
298.20 | 0.4993 | 1.426 |
298.20 | 0.5500 | 1.435 |
298.20 | 0.5995 | 1.408 |
298.20 | 0.6464 | 1.352 |
298.20 | 0.6980 | 1.272 |
298.20 | 0.7453 | 1.184 |
298.20 | 0.7969 | 1.016 |
298.20 | 0.8536 | 0.7680 |
298.20 | 0.9030 | 0.5860 |
298.20 | 0.9500 | 0.3230 |
313.20 | 0.0500 | 0.3390 |
313.20 | 0.0996 | 0.6100 |
313.20 | 0.1496 | 0.8510 |
313.20 | 0.2011 | 1.042 |
313.20 | 0.2515 | 1.198 |
313.20 | 0.3009 | 1.33 |
313.20 | 0.3506 | 1.434 |
313.20 | 0.3988 | 1.509 |
313.20 | 0.4486 | 1.563 |
313.20 | 0.4993 | 1.58 |
313.20 | 0.5500 | 1.575 |
313.20 | 0.5995 | 1.543 |
313.20 | 0.6464 | 1.486 |
313.20 | 0.6980 | 1.387 |
313.20 | 0.7453 | 1.268 |
313.20 | 0.7969 | 1.086 |
313.20 | 0.8536 | 0.8440 |
313.20 | 0.9030 | 0.6020 |
313.20 | 0.9500 | 0.3010 |
328.20 | 0.0500 | 0.3650 |
328.20 | 0.0996 | 0.6730 |
328.20 | 0.1496 | 0.9260 |
328.20 | 0.2011 | 1.146 |
328.20 | 0.2515 | 1.324 |
328.20 | 0.3009 | 1.459 |
328.20 | 0.3506 | 1.572 |
328.20 | 0.3988 | 1.647 |
328.20 | 0.4486 | 1.703 |
328.20 | 0.4993 | 1.709 |
328.20 | 0.5500 | 1.713 |
328.20 | 0.5995 | 1.657 |
328.20 | 0.6464 | 1.591 |
328.20 | 0.6980 | 1.475 |
328.20 | 0.7453 | 1.321 |
328.20 | 0.7969 | 1.163 |
328.20 | 0.8536 | 0.8930 |
328.20 | 0.9030 | 0.6070 |
328.20 | 0.9500 | 0.1980 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0000 | 796.406 |
288.15 | 0.0500 | 841.286 |
288.15 | 0.1000 | 876.23 |
288.15 | 0.1501 | 904.185 |
288.15 | 0.2001 | 926.962 |
288.15 | 0.2501 | 945.901 |
288.15 | 0.3001 | 961.96 |
288.15 | 0.3500 | 975.573 |
288.15 | 0.4001 | 987.417 |
288.15 | 0.4503 | 997.752 |
288.15 | 0.5004 | 1006.896 |
288.15 | 0.5497 | 1014.881 |
288.15 | 0.6000 | 1022.041 |
288.15 | 0.6495 | 1028.476 |
288.15 | 0.6997 | 1034.33 |
288.15 | 0.7978 | 1044.36 |
288.15 | 0.9009 | 1053.152 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 786.987 |
298.15 | 0.0500 | 831.536 |
298.15 | 0.1000 | 866.252 |
298.15 | 0.1501 | 894.037 |
298.15 | 0.2001 | 916.671 |
298.15 | 0.2501 | 935.504 |
298.15 | 0.3001 | 951.502 |
298.15 | 0.3500 | 965.04 |
298.15 | 0.4001 | 976.822 |
298.15 | 0.4503 | 987.12 |
298.15 | 0.5004 | 996.235 |
298.15 | 0.5497 | 1004.184 |
298.15 | 0.6000 | 1011.322 |
298.15 | 0.6495 | 1017.743 |
298.15 | 0.6997 | 1023.585 |
298.15 | 0.7978 | 1033.607 |
298.15 | 0.9009 | 1042.395 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 772.74 |
313.15 | 0.0500 | 816.754 |
313.15 | 0.1000 | 851.13 |
313.15 | 0.1501 | 878.631 |
313.15 | 0.2001 | 901.091 |
313.15 | 0.2501 | 919.763 |
313.15 | 0.3001 | 935.636 |
313.15 | 0.3500 | 949.084 |
313.15 | 0.4001 | 960.784 |
313.15 | 0.4503 | 971.04 |
313.15 | 0.5004 | 980.1 |
313.15 | 0.5497 | 988.016 |
313.15 | 0.6000 | 995.132 |
313.15 | 0.6495 | 1001.516 |
313.15 | 0.6997 | 1007.366 |
313.15 | 0.7978 | 1017.382 |
313.15 | 0.9009 | 1026.218 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 758.201 |
328.15 | 0.0500 | 801.691 |
328.15 | 0.1000 | 835.697 |
328.15 | 0.1501 | 862.956 |
328.15 | 0.2001 | 885.223 |
328.15 | 0.2501 | 903.75 |
328.15 | 0.3001 | 919.517 |
328.15 | 0.3500 | 932.879 |
328.15 | 0.4001 | 944.523 |
328.15 | 0.4503 | 954.725 |
328.15 | 0.5004 | 963.763 |
328.15 | 0.5497 | 971.649 |
328.15 | 0.6000 | 978.761 |
328.15 | 0.6495 | 985.159 |
328.15 | 0.6997 | 991.006 |
328.15 | 0.7978 | 1001.066 |
328.15 | 0.9009 | 1009.978 |
328.15 | 1.0000 | 1017.336 |
Operational condition: Pressure, kPa = 101 (Liquid)
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Mole fraction of Diethyl malonate (1) - Liquid | Mass density, kg/m3 - Liquid |
288.15 | 0.0000 | 796.406 |
288.15 | 0.0500 | 841.286 |
288.15 | 0.1000 | 876.23 |
288.15 | 0.1501 | 904.185 |
288.15 | 0.2001 | 926.962 |
288.15 | 0.2501 | 945.901 |
288.15 | 0.3001 | 961.96 |
288.15 | 0.3500 | 975.573 |
288.15 | 0.4001 | 987.417 |
288.15 | 0.4503 | 997.752 |
288.15 | 0.5004 | 1006.896 |
288.15 | 0.5497 | 1014.881 |
288.15 | 0.6000 | 1022.041 |
288.15 | 0.6495 | 1028.476 |
288.15 | 0.6997 | 1034.33 |
288.15 | 0.7978 | 1044.36 |
288.15 | 0.9009 | 1053.152 |
288.15 | 1.0000 | 1060.326 |
298.15 | 0.0000 | 786.987 |
298.15 | 0.0500 | 831.536 |
298.15 | 0.1000 | 866.252 |
298.15 | 0.1501 | 894.037 |
298.15 | 0.2001 | 916.671 |
298.15 | 0.2501 | 935.504 |
298.15 | 0.3001 | 951.502 |
298.15 | 0.3500 | 965.04 |
298.15 | 0.4001 | 976.822 |
298.15 | 0.4503 | 987.12 |
298.15 | 0.5004 | 996.235 |
298.15 | 0.5497 | 1004.184 |
298.15 | 0.6000 | 1011.322 |
298.15 | 0.6495 | 1017.743 |
298.15 | 0.6997 | 1023.585 |
298.15 | 0.7978 | 1033.607 |
298.15 | 0.9009 | 1042.395 |
298.15 | 1.0000 | 1049.603 |
313.15 | 0.0000 | 772.74 |
313.15 | 0.0500 | 816.754 |
313.15 | 0.1000 | 851.13 |
313.15 | 0.1501 | 878.631 |
313.15 | 0.2001 | 901.091 |
313.15 | 0.2501 | 919.763 |
313.15 | 0.3001 | 935.636 |
313.15 | 0.3500 | 949.084 |
313.15 | 0.4001 | 960.784 |
313.15 | 0.4503 | 971.04 |
313.15 | 0.5004 | 980.1 |
313.15 | 0.5497 | 988.016 |
313.15 | 0.6000 | 995.132 |
313.15 | 0.6495 | 1001.516 |
313.15 | 0.6997 | 1007.366 |
313.15 | 0.7978 | 1017.382 |
313.15 | 0.9009 | 1026.218 |
313.15 | 1.0000 | 1033.498 |
328.15 | 0.0000 | 758.201 |
328.15 | 0.0500 | 801.691 |
328.15 | 0.1000 | 835.697 |
328.15 | 0.1501 | 862.956 |
328.15 | 0.2001 | 885.223 |
328.15 | 0.2501 | 903.75 |
328.15 | 0.3001 | 919.517 |
328.15 | 0.3500 | 932.879 |
328.15 | 0.4001 | 944.523 |
328.15 | 0.4503 | 954.725 |
328.15 | 0.5004 | 963.763 |
328.15 | 0.5497 | 971.649 |
328.15 | 0.6000 | 978.761 |
328.15 | 0.6495 | 985.159 |
328.15 | 0.6997 | 991.006 |
328.15 | 0.7978 | 1001.066 |
328.15 | 0.9009 | 1009.978 |
328.15 | 1.0000 | 1017.336 |